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Anhui Liwei Chemical Co., Limited.

SELVOL Polyvinyl Alcohol 540

    • Product Name: SELVOL Polyvinyl Alcohol 540
    • Factroy Site: Lingwu, Yinchuan, Ningxia, China
    • Price Inquiry: sales2@liwei-chem.com
    • Manufacturer: Anhui Liwei Chemical Co., Limited.
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    Specifications
    HS Code 253492
    Product Name SELVOL Polyvinyl Alcohol 540
    Cas Number 9002-89-5
    Chemical Formula (C2H4O)n
    Appearance White to cream granular powder
    Degree Of Hydrolysis 87.0 - 89.0 mol%
    Viscosity 4 Solution At 20 C 45 - 55 cP
    Ph 4 Aqueous Solution 5.0 - 7.0
    Ash Content ≤ 1.0%
    Moisture Content ≤ 5.0%
    Bulk Density 0.45 - 0.60 g/cm³
    Solubility Soluble in water; solubility increases with temperature
    Glass Transition Temperature Approximately 70°C
    Melting Point Approximately 190°C
    Specific Gravity 1.27 - 1.31

    As an accredited SELVOL Polyvinyl Alcohol 540 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing SELVOL Polyvinyl Alcohol 540 is a free-flowing white powder supplied in 25 kg multi-wall paper bags with a polyethylene liner.
    Container Loading (20′ FCL) 20′ FCL loading of SELVOL Polyvinyl Alcohol 540: palletized 25kg bags, securely stowed, protected from moisture and damage.
    Shipping SELVOL Polyvinyl Alcohol 540 is shipped as a non-hazardous, water-soluble powder in multiwall paper bags or fiber drums, palletized and stretch-wrapped. Keep sealed, dry, and away from ignition sources, as dust may form combustible mixtures. Avoid moisture exposure to prevent clumping and product degradation.
    Storage Store SELVOL Polyvinyl Alcohol 540 in a cool, dry, well-ventilated area, away from moisture, heat, sparks, and open flames. Keep the original container tightly closed when not in use to prevent dust accumulation and contamination. Avoid contact with oxidizing agents. Ensure proper labeling and segregate from incompatible materials.
    Shelf Life Store in a cool, dry place in original sealed container. Shelf life is two years from date of manufacture.
    Application of SELVOL Polyvinyl Alcohol 540

    Alkaline fine-paper manufacturing that operates a rod-metered film press at 450-600 m/min requires a size press fluid with controlled extensional viscosity to avoid misting while maintaining surface strength on 70-90 g/m² base sheet. Selvol Polyvinyl Alcohol 540, with 4% aqueous solution viscosity of 45.0-55.0 mPa·s at 20°C and hydrolysis between 87.0-89.0 mol%, is dissolved in a jacketed batch tank at 85-90°C for 30-45 minutes under low-shear agitation, then filtered through a 100 µm screen before letdown. The size press recipe uses the cooked 15.0% solution diluted to 5.0-8.0% solids and applies 0.5-1.2 g/m² dry deposition per side, replacing 20-35% of oxidized corn starch solids in a blend. ISO 3783 IGT surface strength and ISO 535 Cobb water absorption are the relevant release test methods; the 540 grade raises IGT pick resistance but narrows the running window compared with a lower-viscosity partially hydrolysed grade. When use solids exceed 8.5% and application temperature drops below 60°C, mill-scale film presses have shown shear-induced misting and metering rod stringing; below 5.0% solids, film uniformity on lightweight sheets below 60 g/m² is insufficient. After the size press, drying cylinders are run with surface temperatures of 100-120°C; the resulting base sheets are converted into copy paper, offset printing grades, and envelope stock. For food-contact paper and paperboard, the polymer is evaluated under FDA 21 CFR 176.170 and FDA 21 CFR 176.180; in EU markets, food-contact compliance is assessed under Commission Regulation (EU) No 10/2011 Annex I with overall migration testing per EN 1186-1.

    Which Reactor Feed Strategy Prevents Localised Gel Bodies in VAE Protective Colloid Systems?

    In vinyl acetate-ethylene copolymerisation, protective colloid performance is governed by hydrolysis distribution, block character, and solution rheology. Selvol 540 at 87.0-89.0 mol% hydrolysis and 45.0-55.0 mPa·s 4% viscosity stabilises monomer droplets in a jacketed stirred-tank reactor equipped with a turbine or anchor agitator running at 30-60 rpm. Reaction temperature is controlled between 60-85°C and ethylene pressure between 20-50 bar for an 80:20 vinyl acetate:ethylene mass ratio. The polymer is pre-dissolved in a separate vessel at 15.0% solids and 85°C for 30 minutes; it is then fed into the reactor at 2.0-5.0 wt% based on total vinyl acetate and ethylene monomer, with a tight commercial operating envelope of 3.0-3.5 wt%. Higher colloid additions raise latex viscosity and may require post-reaction dilution to bring the batch within 500-3,000 mPa·s when measured by Brookfield RVT spindle 4 at 20 rpm and 25°C. Production-scale operators have observed that feeding the colloid solution below the liquid surface at stream temperatures below 20°C forms localised gel bodies; an above-surface metered feed or pre-dilution to 10.0% prevents this failure mode. Initiation is by a redox pair of persulphate and sodium metabisulphite, with pH maintained at 4.0-5.5; after reaching 95-99% conversion, residual vinyl acetate is reduced by a thermally activated persulphate chase at 80°C. The resulting VAE emulsions are formulated into wood flooring adhesives, paperboard packaging adhesives, and nonwoven binders. For these end uses, the adhesive film or coated substrate is assessed under FDA 21 CFR 175.105, FDA 21 CFR 176.170, and FDA 21 CFR 176.180; EU users rely on Regulation (EC) No 1907/2006 REACH registration data and, where food contact applies, Commission Regulation (EU) No 10/2011.

    When cotton and cotton/polyester yarns are slashed for high-speed air-jet weaving at 700-1,000 rpm, the warp size film must withstand repeated lease-rod friction without dusting or loss of weaving efficiency. Selvol Polyvinyl Alcohol 540 is incorporated at 30-50% of total size solids in a cooked size mix at 8.0-12.0% final solids; the 540 portion is prepared separately at 15.0% solids and then blended with the starch cook. Add-on is controlled between 6.0-10.0% of warp yarn dry weight depending on yarn count, twist, and fibre blend. In the slasher size box, the bath is held at 70-80°C, and squeeze roll pressure is set between 10-30 kN across the roll width to meet the target wet pickup; drying cylinders downstream are operated at 100-125°C surface temperature with final yarn moisture below 8.0%. The medium-viscosity 540 produces a higher-tensile size film than low-viscosity partially hydrolysed grades, but the return size circuit must avoid excessive turbulence because shear-induced foam accumulates at the size box and creates uneven pick-up across the warp sheet. Boric acid or borax is omitted from formulations based on 540 because gelation sharply increases apparent size-bath viscosity and complicates box level control. Desizing on downstream finishing lines is performed in water at 80°C or above; incomplete removal before bleaching or reactive dyeing lowers absorbency and produces uneven dye uptake. Terminal products include woven apparel fabrics, workwear fabrics, and home textile base cloth. Mills supplying OEKO-TEX Standard 100 articles must confirm that the desizing and scouring process removes the polymeric film below the relevant residue limit; at the chemical supply level, EU users operate under Regulation (EC) No 1907/2006 REACH obligations.

    Remoistenable Adhesive Films for Envelope and Paper-Tape Converting Lines

    In remoistenable adhesive coating, a continuous polyvinyl alcohol film is applied to one side of a paper web and dried to a non-blocking surface that recovers tack upon water rewetting. Selvol Polyvinyl Alcohol 540 is prepared as a 15.0-25.0% aqueous solution at 85-90°C; after cooling to 40-50°C, plasticizer is incorporated at 5-15 phr of dry polymer mass, commonly glycerol or sorbitol syrup. The coating line consists of a direct gravure or reverse-roll coater operating at 30-50 m/min and a drying tunnel with air temperatures from 60-80°C. Dry film coat weight is specified between 4.0-8.0 g/m² on one surface. Application viscosity is normally 500-4,000 mPa·s; when viscosity exceeds 4,000 mPa·s, gravure transfer becomes irregular and ribbing appears on the coated web. After drying, rewetting speed is measured on a laboratory moistening wheel to verify tack development within 5-15 seconds. Terminal products include postage-stamp sheets, envelope flaps, paper tape closures, and label papers. For adhesives used in indirect food-contact applications, compliance is assessed under FDA 21 CFR 175.105 for adhesive components and FDA 21 CFR 176.180 if coated onto food-contact paper or paperboard. EU users should verify polymer compliance under Commission Regulation (EU) No 10/2011 when the final article is intended for food contact. Unwrapped coated sheets stored at relative humidity above 70% block; interleaving with silicone-treated paper or sealed film overwrap is required for tropical shipment. Residual moisture above 8.0% at the drying tunnel exit causes adhesive transfer to the metering roll on subsequent batches.

    When 540 PVOH Is Dry-Blended into Gypsum-Based Joint and Patch Compounds without Prior Solution Preparation

    In dry-mix gypsum compounds, Selvol Polyvinyl Alcohol 540 added as a dry powder at 0.3-0.8 wt% of total batch mass modifies water retention, open time, and adhesion to paper tape without requiring a separate polymer solution tank. The powder is charged into a ribbon or ploughshare blender with gypsum hemihydrate and limestone fillers; dry blending time is 10-20 minutes at 20-50 rpm. Batch sizes above 1,500 kg in horizontal ploughshare mixers require extended blending to maintain coefficient of variation below 5.0% on the polymer content. The compound is then mixed with potable water at 40-50 parts water per 100 parts dry powder and applied by hand trowel or airless spray. The solution viscosity of 540 in the aqueous phase slows water migration into the porous gypsum substrate; above 0.8 wt%, trowel drag increases and hardening time is extended, while below 0.3 wt% no measurable change in sag resistance is observed under ASTM C474. Terminal products are gypsum joint compounds, patching plasters, and interior texturing compounds applied over gypsum wallboard. Compliance is verified through ASTM C474 for joint compound properties, ASTM C475 for joint tape, and ASTM C1396/C1396M for gypsum board assemblies. EU users placing the dry mix on the market must meet Regulation (EC) No 1907/2006 REACH and, where applicable, national formaldehyde emission regulations; the polymer itself is not a formaldehyde source but may interact with formaldehyde-scavenging additives if not uniformly dispersed. The dry-blend route avoids installing a separate polymer solution tank, but the dry addition must be validated for lot-to-lot variability because particle size distribution of the polymer affects low-shear mixing dispersion in the field.

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    Certification & Compliance
    More Introduction

    SELVOL Polyvinyl Alcohol 540 is a partially hydrolyzed polyvinyl alcohol resin supplied as a white to off-white granular powder. It is a copolymer of vinyl alcohol and residual vinyl acetate, not a fully saponified homopolymer, and the residual acetate content is the structural feature that differentiates the partially hydrolyzed SELVOL series from fully hydrolyzed grades. The product is defined by a 4% aqueous solution viscosity of 45.0–55.0 mPa·s at 20°C, a degree of hydrolysis of 87.0–89.0 mol%, and a solution pH of 4.5–6.5. Volatile matter is controlled to ≤5.0% and ash to ≤0.5% as Na2O. These specifications place SELVOL 540 in the upper viscosity range of partially hydrolyzed SELVOL grades; it is distinguished from SELVOL 523 by roughly a twofold higher solution viscosity and from SELVOL 205 by roughly ninefold higher solution viscosity at equal solids.

    Because the hydrolysis window is 87.0–89.0 mol%, the polymer backbone contains acetate side groups that suppress crystallinity relative to fully hydrolyzed SELVOL 107 at 98.0–99.0 mol% hydrolysis. This reduces the onset temperature for hydration and permits dissolution in cold water at a rate not attainable with the fully hydrolyzed grade. The higher viscosity of SELVOL 540 at 45.0–55.0 mPa·s is a consequence of longer chain structure; the value is not a melt-flow parameter but a low-solids solution viscosity measurement used for grade differentiation and incoming inspection.

    The specification values used for incoming inspection are shown in Table 1. The reference test methods are based on JIS K6726 and are cross-checked against ISO 15023-1 designation guidance.

    PropertyReference methodSpecified range
    Viscosity of 4% aqueous solution at 20°CJIS K672645.0–55.0 mPa·s
    Degree of hydrolysisJIS K672687.0–89.0 mol%
    pH of 4% solution at 20°CJIS K67264.5–6.5
    Volatile matterJIS K6726≤5.0%
    Ash as Na2OJIS K6726≤0.5%

    What limits dissolution time and solution clarity in partially hydrolyzed PVOH?

    Production dissolution of SELVOL 540 is limited by particle wetting, shear history, and the final heating ramp. A frequent procedure is to charge cold water at 10–20°C into a jacketed vessel, add the resin through an eductor or under a high-shear Cowles disperser, and heat the slurry at 1–2°C/min to 88–92°C. The vessel is held at temperature for 30–45 min. Direct addition of dry powder to hot water is not used because rapid hydration forms gelatinous skins around undissolved granules; those agglomerates subsequently blind filter screens and reduce solution clarity. A deep vortex should be avoided because entrained air stabilizes foam and retards wetting.

    Once cooled to 20°C, a 4% solution is checked with a Brookfield RV-type rotational viscometer fitted with a UL adapter at 20 rpm. If the measured viscosity is outside 45.0–55.0 mPa·s, the cause is normally solids error, incomplete hydration, shear degradation, or chemical hydrolysis during the cook. The solution is normally filtered through a 100 µm bag filter or finer cartridge if used for gravure coating. Haze can originate from hard water cations, microbial growth, or aging at low temperature; storage is normally kept above 5°C. In closed stainless steel tanks, neutral aqueous PVOH should be used within a validated hold time or protected with a biocide selected for the end use.

    SELVOL 540 behaves as a near-Newtonian solution at 4% solids, but the rheology becomes pseudoplastic as concentration increases toward the 20–30% solids range used in adhesives. At those higher solids, a Brookfield reading at 20 rpm is insufficient for pump sizing and transfer-line pressure drop; capillary or cone-plate data at the intended shear rate is required. The higher molecular weight of SELVOL 540 shifts the onset of significant shear thinning to lower concentrations than SELVOL 523, which must be considered when changing grades in an existing mixing and coating system.

    In remoistenable adhesive formulations, SELVOL 540 is cooked at 20–30% solids and applied by roll, rod, or direct gravure coating. The high viscosity grade increases dried film toughness and slows rewetting compared with SELVOL 523, a property that is relevant when a water-wheel on an envelope line contacts the adhesive for less than one second. Production lines running at 150–250 m/min require rapid wet tack development; converter evaluations are performed at 23°C and 50% RH using ASTM D1876 T-peel on kraft paper. Open time is controlled by humectant level, often a glycol or sorbitol, because PVOH itself is not the primary open-time modifier.

    The 45.0–55.0 mPa·s base viscosity allows higher water dilution while maintaining transfer control on a direct gravure coater, but it raises pressure drop in heated transfer lines and may require positive-displacement pumps instead of centrifugal pumps. Plasticizer selection is common. Glycerin, sorbitol, or polyethylene glycol reduces film brittleness and lowers blocking tendency on stacked blanks, but plasticizer migration under storage at 40°C and 70% RH can change wet tack. The plasticizer-to-PVOH ratio is typically adjusted between 5 and 30 phr; the optimum depends on paper porosity and coating weight. Batch-to-batch viscosity variation within the 45.0–55.0 mPa·s specification window is normally narrow, but a shift of a few millipascal-seconds at 4% solids can be amplified at 20–30% solids and alter coat weight.

    Emulsion polymerization stabilizer performance is governed by hydrolysis distribution and molecular weight.

    SELVOL 540 serves as a protective colloid in vinyl acetate homopolymer and vinyl acetate-ethylene emulsion polymerization. The partially hydrolyzed structure is the controlling parameter: the 87.0–89.0 mol% hydroxyl content provides aqueous solubility, while the residual acetate segments increase adsorption onto polyvinyl acetate particle surfaces. During polymerization, radicals abstract hydrogen from the PVOH backbone and graft growing chains to the stabilizer. This grafted layer anchors the colloid to the latex particle and supplies the steric barrier that reduces shear-induced coagulation. Grafting yield is governed by initiator type, addition rate, and temperature; published data for this specific SELVOL 540 configuration is limited, so reactor qualification is normally based on particle size distribution, latex viscosity, and coagulum formation rather than grafting efficiency.

    The high molecular weight of SELVOL 540 raises the low-shear latex viscosity more than an equal mass concentration of SELVOL 523. In a batch reactor with a pitched-blade turbine or an anchor impeller, raising protective colloid from 2.0 to 5.0 wt% on monomer can shift Brookfield viscosity from several hundred to several thousand millipascal-seconds. When the reactor agitator is already near torque limits, SELVOL 540 may force a lower maximum solids or a change to SELVOL 523 to preserve heat-transfer capacity. Latex particle size is measured with ISO 22412 dynamic light scattering or ISO 13320 laser diffraction; higher colloid concentration normally narrows the particle size distribution, but the optimum is a compromise between coagulation resistance and downstream pumping and spray-drying.

    Buffer and salt tolerance define further boundaries. Sodium bicarbonate buffers used in VAE polymerization alter ionic strength and may reduce stabilizer solubility if dosed too rapidly. Hard water containing divalent cations can form complexes with residual acetate groups and create reactor-wall coagulum. Extended temperature excursions above 90°C during the hold period can hydrolyze residual acetate groups and shift the effective stabilizer composition; operators monitor pH, torque, and jacket temperature for early detection.

    In textile warp sizing, SELVOL 540 is prepared at 8–14% solids in a jacketed kettle and applied in the size box of a slasher line at 60–120 m/min. Squeeze-roll pressure and size-box temperature are adjusted to control add-on; the high-viscosity grade forms a tougher size film under weaving tensions than SELVOL 523 at equal add-on. Yarn breakage is assessed by loom stop counts rather than by a single universal standard. Hot-water desizing at 80–90°C with nonionic surfactant removes the film; the partially hydrolyzed structure swells faster than fully hydrolyzed PVOH, reducing desize cycle time.

    In surface sizing of paper and paperboard, SELVOL 540 is dosed into the size-press solution at 0.5–2.0 wt%. The high molecular weight raises oil and grease resistance and film strength at low coat weights, but it can reduce runnability if the size-press viscosity exceeds the metering range of the rod or film-press unit. Mill trials compare grades using ISO 535 Cobb water absorption and TAPPI T 559 kit-level grease resistance. Because SELVOL 540 produces higher solution viscosity than SELVOL 523 at equal solids, it can be run at lower solids when dryer capacity is constrained.

    Another usage where the grade is evaluated is water-soluble film casting for detergent sachets or agrochemical packaging. The casting solution at 10–15% solids is deaerated under vacuum and held at 60–70°C in a jacketed feed tank. Slot-die casting requires filtration through a 40 µm cartridge because gel particles and undissolved resin create die streaks. Partially hydrolyzed grades dissolve faster in cold water than fully hydrolyzed films, but the high viscosity of SELVOL 540 increases die-back pressure and can reduce casting speed when compared with SELVOL 523. Published data for this specific SELVOL 540 configuration in water-soluble film is limited; film solubility is normally qualified by a water-disintegration test at 10°C and 20°C using the end user’s specified laboratory shaker method.

    Cast films of SELVOL 540 are evaluated with ISO 527-3 after conditioning at 23°C and 50% RH. The higher solution viscosity grade generally produces higher tensile strength and modulus than SELVOL 523 at equal thickness and plasticizer content. Elongation at break is controlled mainly by plasticizer content and equilibrium moisture. Because published tensile data for this specific grade is limited, comparative film testing should be conducted under the same conditioning and casting protocol instead of using generic PVOH literature values.

    When SELVOL 540 replaces fully hydrolyzed grades in barrier coatings and water-resistant adhesives

    SELVOL 540 is not a drop-in replacement for fully hydrolyzed PVOH when water resistance of the uncrosslinked film is the primary specification. Fully hydrolyzed SELVOL 107 at 98.0–99.0 mol% hydrolysis develops higher crystallinity after drying and lower solubility after thermal annealing at 150–180°C. A partially hydrolyzed film remains more water-sensitive because the residual acetate groups reduce the driving force for crystallite formation. Grade selection therefore depends on whether cold-water solubility or final water resistance is the dominant process constraint.

    When SELVOL 540 is used in a water-resistant adhesive or coating, insolubilization is achieved with glyoxal, glyoxylic acid resin, or a suitable multivalent metal salt. Glyoxal is typically added at 0.5–2.0 wt% of PVOH solids and requires a curing step above 100°C to approach full insolubilization. Pot life of a glyoxal-crosslinked solution is limited; viscosity increases with time and pH, and the batch should be applied within the validated working window. Borate salts gel the aqueous solution at levels often below 0.1 wt%, which precludes spray application but is useful for temporary protective films and remoistenable debonding. Strong oxidizing agents such as hypochlorite are incompatible because they cause chain scission and reduce viscosity.

    Table 2 compares SELVOL 540 with adjacent grades across the specification variables used for grade selection. SELVOL 205, SELVOL 523, and SELVOL 540 share the 87.0–89.0 mol% hydrolysis band, so solution viscosity is the primary differentiating property. Fully hydrolyzed SELVOL 107 differs in both hydrolysis and low-temperature solubility.

    GradeViscosity of 4% aqueous solution at 20°CHydrolysisPrimary selection difference
    SELVOL 2055.0–6.0 mPa·s87.0–89.0 mol%Low viscosity, easier spray and higher solids
    SELVOL 52323.0–27.0 mPa·s87.0–89.0 mol%Intermediate viscosity, lower torque in mixers
    SELVOL 54045.0–55.0 mPa·s87.0–89.0 mol%Higher film strength and thicker solution rheology
    SELVOL 1076.0–8.0 mPa·s98.0–99.0 mol%Fully hydrolyzed; lower cold-water solubility, higher water resistance after drying

    For food-contact adhesives and paper and paperboard applications, SELVOL PVOH grades are generally evaluated against 21 CFR 175.105, 21 CFR 176.170, and 21 CFR 176.180. The converter must confirm finished-article compliance under the intended use conditions; supplier food-contact statements are lot-specific and regulatory jurisdiction-specific. EU REACH registration status and residual monomer data are specified in the extended safety data sheet.

    Storage boundaries are operational rather than cosmetic. Bags should be kept closed below 60% RH. Moisture absorption above 5.0% alters the effective solids content of aqueous batches and can cause bridging in gravimetric feeders. In high-humidity operations, pre-drying at 40–50°C for 2–4 h may be required before weighing. The powder is combustible; dust control and grounding are handled according to NFPA 652 or equivalent plant protocols.